Copolyester resin composition and a process of preparation thereof
a technology of copolyester resin and resin composition, which is applied in the field of copolyester resin composition and a process, can solve the problems of poor physical properties and inferior processability, limited use of this polymer material, and serious environmental concerns in the world
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example 1
[0035] First, after purging a 500 ml reactor with nitrogen, 23.6 g of succinic acid, 27 g of 1,4-butanediol, and 0.1 g of tetrabutyl titanate acting as a catalyst are added to a reactor, and the mixture is esterification reacted until the approximate theoretical amount of water is produced at the temperature of 205.degree. C. After water is extracted, 34.4 g of "aliphatic prepolymers", wherein the number average molecular weight of "aliphatic prepolymers" is approximately 600, is obtained.
[0036] And then, 77.7 g of dimethyl terephthalate, 135.2 g of 1,4-butanediol, 0.2 g of tetrabutyl titanate acting as a catalyst are added thereto, and the mixture is ester-exchange reacted until the approximate theoretical amount of methanol is produced at the temperature of 205.degree. C. After the methanol is extracted, 35.4 g of succinic acid and 43.8 g of adipic acid are added thereto, and the mixture is esterification reacted until the approximate theoretical amount of water is produced at the...
example 2
[0041] First, after purging a 500 ml reactor with nitrogen, 2.95 g of succinic acid, 3.65 g of adipic acid, 6.3 g of 1,4-butanediol, and 0.1 g of tetrabutyl titanate acting as a catalyst are added to a reactor, and the mixture is esterification reacted until the approximate theoretical amount of water is produced at the temperature of 205.degree. C. After water is extracted, 9.3 g of "aliphatic prepolymers", wherein the number average molecular weight of "aliphatic prepolymers" is approximately 1,500, is obtained.
[0042] And then, 78.8 g of dimethyl terephthalate, 126 g of 1,4-butanediol, 6.2 g of ethylene glycol, and 0.2 g of tetrabutyl titanate acting as a catalyst are added thereto, and the mixture is ester-exchange reacted until the approximate theoretical amount of methanol is produced at the temperature of 205.degree. C. After the methanol is extracted, 70.8 g of succinic acid is added thereto, and the mixture is esterification reacted until the approximate theoretical amount o...
example 3
[0047] First, after purging a 500 ml reactor with nitrogen, 2.95 g of succinic acid, 2.48 g of ethylene glycol, and 0.1 g of tetrabutyl titanate acting as a catalyst are added to a reactor, and the mixture is esterification reacted until the approximate theoretical amount of water is produced at the temperature of 205.degree. C. After water is extracted, 3.6 g of "aliphatic prepolymers", wherein the number average molecular weight of "aliphatic prepolymers" is approximately 400, is obtained.
[0048] And then, 108.4 g of dimethyl terephthalate, 135.2 g of 1,4-butanediol, and 0.2 g of tetrabutyl titanate acting as a catalyst are added thereto, and the mixture is ester-exchange reacted until the approximate theoretical amount of methanol is produced at the temperature of 205.degree. C. After the methanol is extracted, 53.1 g of succinic acid is added thereto, and the mixture is esterification reacted until the approximate theoretical amount of water is produced at the temperature of 180....
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